User Manual
6
All Rights Reserved. Copyright © 2011, Yokogawa Electric Corporation. Subject to change without notice. April 2011IM 11A00V01-01E-A
This section of the manual describes the basic theory of operation, designed to give the user a better understanding and
help in operation and maintenance.
3.1 Brief History of Reux Samplers
The concept of the Reux Sampler was introduced in mid 1970’s and until the inception of the Advanced Reux Sampler
(YARS), it had changed very little. Process analysis needs during the mid 1970’s were not as critical as they are now and
consequently, the Reux Samplers designed previously no longer meet today’s demands that are more stringent. The
reux sampler was originally designed to overcome the problem of constantly plugging sample probes installed on the
Transfer Line Exchangers (TLE) of ethylene cracking furnace euents. This high temperature cracked gas euent is high
in particulate and condensables (moisture and heavy hydrocarbons) content and therefore prone to plugging. The idea
that the condensables could be used to backwash a particulate lter was conceived and a Reux Sampler was then
developed. A simple lter mesh was used to trap the particulate matter.
3.2 Filter Section
The lower section of the YARS is for particulate ltration and provides some primary sample cooling. Typically ange
mounted directly to a customer supplied process isolation valve and ange mounted to the heat exchanger section of
the YARS. The lter media is nominally stainless steel wire mesh that traps any particulate matter such as coke from the
ethylene furnaces and/or catalyst nes. During normal operation, the temperature at the lter section outlet should be
in the order of 120
o
F (50
o
C), indicating a balanced reuxing condition is established. This lter section is cooled by the
condensate that has dropped out from the heat exchanger mounted directly above the lter. The condensate also acts as
a trap for ner particulate matter. In certain environmental conditions where sub-zero temperatures are anticipated, it may
be desirable to insulate the lter section. This will prevent premature condensing and allow for a balanced reuxing action.
3.3 Steam Supplement
For the YARS to function reliably there must be sucient quantity of condensable media in the sample. For applications
that have high particle loading and limited condensables present, steam should be added at the inlet. The YARS lter
section has a steam inlet facility located at the inlet. A suitably rated needle valve is provided for regulating a nominal ow
of steam in to the lter section via an inverted tube such that the steam is directed up in to the lters. Note that the steam
is added directly to the sample and therefore the composition will be aected the H
2
O addition. As each application has
many dierent operating parameters, there are no specic settings for the quantity of steam addition and each application
is set-up individually.
3.4 Inlet Temperature Section
Mounted between the lter and heat exchanger section is the inlet temperature thermowell. As standard, a suitable
temperature gauge is installed in the thermowell. The purpose of temperature measurement at this point in the YARS is
to help establish the correct temperature gradient required for reuxing. The two undesirable conditions within the ler
section are as below:
• Temperature reading too high – will cause the heat exchanger to work excessively and indicates a problem
elsewhere in the system
• Temperature reading too low – will cause the condensable media to dropout early in the lter section and not
provide proper lter cleansing by reux.
When troubleshooting the YARS, consider the correct temperature at this point.
3.5 Heat Exchanger Section
This is truly unique to the YARS in many respects. This section provides the cooling of the sample and is most critical to
the overall operation. As the sample gas rises from the lter section, through the inlet temperature section, it is channeled
in to the heat exchanger chamber. The sample gas rises through a chamber in which the cooling coils are concentrically
mounted. The design of the heat exchanger is such that maximum surface area contact between the cooling coils and
3. THEORY OF OPERATION